CN111721150A - A compact multi-stage series PCHE heat exchanger and heat exchange method - Google Patents
A compact multi-stage series PCHE heat exchanger and heat exchange method Download PDFInfo
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- CN111721150A CN111721150A CN202010730018.2A CN202010730018A CN111721150A CN 111721150 A CN111721150 A CN 111721150A CN 202010730018 A CN202010730018 A CN 202010730018A CN 111721150 A CN111721150 A CN 111721150A
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- 238000000034 method Methods 0.000 title claims abstract description 8
- DDTVVMRZNVIVQM-UHFFFAOYSA-N 2-(1-azabicyclo[2.2.2]octan-3-yloxy)-1-cyclopentyl-1-phenylethanol;hydrochloride Chemical compound Cl.C1N(CC2)CCC2C1OCC(O)(C=1C=CC=CC=1)C1CCCC1 DDTVVMRZNVIVQM-UHFFFAOYSA-N 0.000 title claims abstract 6
- 238000010248 power generation Methods 0.000 claims abstract description 6
- 239000000498 cooling water Substances 0.000 claims description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000002184 metal Substances 0.000 claims description 3
- 238000009792 diffusion process Methods 0.000 claims description 2
- 238000005530 etching Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 10
- 238000001816 cooling Methods 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0006—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the plate-like or laminated conduits being enclosed within a pressure vessel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0037—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
- F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0093—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/048—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本发明公开了一种紧凑型多级串联PCHE换热器及换热方法,所述换热器包括,回热器,预冷器以及连接管道,具体的回热器和预冷器包括各自的前盖板、若干热介质板片、冷介质板片和后盖组成,热介质板片和冷介质板片上的微通道采用蚀刻加工而成,该换热器以圆筒形为空间限制,以超临界CO2发电系统为应用背景,集成了超临界CO2发电系统中回热器与预冷器的功能,该换热器系统最大限度的有效利用给定空间。
The invention discloses a compact multi-stage series PCHE heat exchanger and a heat exchange method. The heat exchanger includes a regenerator, a precooler and a connecting pipeline. The specific regenerator and the precooler include respective The front cover plate, several heat medium plates, cold medium plates and back cover are composed. The microchannels on the heat medium plates and the cold medium plates are processed by etching. The supercritical CO2 power generation system is the application background, which integrates the functions of the regenerator and the precooler in the supercritical CO2 power generation system. The heat exchanger system maximizes the effective use of the given space.
Description
技术领域technical field
本发明属于换热装置技术领域,涉及一种紧凑型多级串联PCHE换热器及换热方法。The invention belongs to the technical field of heat exchange devices, and relates to a compact multi-stage series-connected PCHE heat exchanger and a heat exchange method.
背景技术Background technique
印刷电路板式换热器(printed circuit heat exchanger,PCHE)属于微通道板式换热器范畴。PCHE具有结构紧凑、耐高温、耐高压、安全可靠等优点,在制冷空调、石油天然气、核工业、化工工业、电力工业等领域应用广泛。Printed circuit heat exchanger (PCHE) belongs to the category of microchannel plate heat exchanger. PCHE has the advantages of compact structure, high temperature resistance, high pressure resistance, safety and reliability, etc. It is widely used in refrigeration and air conditioning, oil and gas, nuclear industry, chemical industry, power industry and other fields.
目前常见的PCHE换热器多为方形,且进出口管口分布在换热器上4 个不同侧面,这样换热器进出口管道比较分散,占据空间较大。另外,一般来说一个PCHE换热器只实现一个回路的换热器功能,几个回路多次换热需要多个独立的PCHE换热器来实现,这样会出现更多的换热器进出口连接管,占据更多空间。At present, the common PCHE heat exchangers are mostly square, and the inlet and outlet pipes are distributed on 4 different sides of the heat exchanger, so that the inlet and outlet pipes of the heat exchanger are scattered and occupy a large space. In addition, in general, a PCHE heat exchanger only realizes the heat exchanger function of one loop, and multiple independent PCHE heat exchangers are required to achieve multiple heat exchanges in several loops, so that there will be more heat exchanger inlets and outlets. Connect the tubes to take up more space.
在某些特殊应用场合,例如舰船、海上平台等,由于空间狭小,且对布置形状有特殊要求时,普通的方形独立PCHE换热器空间利用率太低,需要特殊设计的换热器来满足特殊需求。In some special applications, such as ships, offshore platforms, etc., due to the narrow space and special requirements for the layout shape, the space utilization rate of the ordinary square independent PCHE heat exchanger is too low, and a specially designed heat exchanger is required to Meet special needs.
发明内容SUMMARY OF THE INVENTION
为了解决以上现有技术存在的问题,本发明的目的在于提供一种适用于圆筒形布置要求的紧凑式串联PCHE换热器及换热方法,以超临界CO2 循环发电系统为应用背景,该换热器以圆筒形布置为空间布置要求,这样的布置最大限度的利用了圆柱形空间,满足圆柱形空间布置的特殊需求。In order to solve the above problems existing in the prior art, the purpose of the present invention is to provide a compact series PCHE heat exchanger and a heat exchange method suitable for the requirement of cylindrical arrangement. Taking the supercritical CO2 cycle power generation system as the application background, the The heat exchanger is arranged in a cylindrical shape as the space layout requirement. This arrangement maximizes the use of the cylindrical space and meets the special needs of the cylindrical space layout.
为实现上述目的,本发明采用的技术方案如下:For achieving the above object, the technical scheme adopted in the present invention is as follows:
一种紧凑型多级串联PCHE换热器,所述换热器系统能够实现超临界 CO2发电系统中回热器与预冷器的功能,整体呈圆柱状,该系统包括回热器、预冷器、进出口管道及连接管;所述回热器包括从前到后依次焊接连接为整体的回热器前盖板1.1、若干回热器冷介质板片1.2、若干回热器热介质板片1.3和回热器后盖板1.4,所述预冷器包括从前到后依次焊接连接为整体的预冷器前盖板2.1、若干预冷器热介质板片2.2、若干预冷器冷介质板片2.3和预冷器后盖板2.4,所述进出口管道包括回热器热侧入口管道 3、预冷器热侧出口管道5、回热器冷侧出口管道6、回热器冷侧入口管道 7、冷却水出口管道8和冷却水入口管道9,所述连接管为回热器热侧出口 -预冷器热侧入口连接管4,所述回热器和预冷器通过回热器热侧出口-预冷器热侧入口连接管4连接在一起;所述回热器冷介质板片1.2、回热器热介质板片1.3、预冷器热介质板片2.2、预冷器冷介质板片2.3均为金属板面上蚀刻微通道的板片,所述回热器冷介质板片1.2和回热器热介质板片1.3间隔分布,所述预冷器热介质板片2.2和回热器冷介质板片2.3间隔分布;A compact multi-stage series PCHE heat exchanger, the heat exchanger system can realize the functions of a regenerator and a precooler in a supercritical CO2 power generation system, and the whole is cylindrical, and the system includes a regenerator, a precooler The regenerator includes a regenerator front cover 1.1, a number of regenerator cold medium plates 1.2, and a number of regenerator heat medium plates that are welded and connected as a whole from front to back. 1.3 and the rear cover plate 1.4 of the regenerator, the pre-cooler includes a pre-cooler front cover plate 2.1, a number of pre-cooler heat medium plates 2.2, a number of pre-cooler cold medium plates that are welded and connected as a whole from front to back. Sheet 2.3 and precooler rear cover plate 2.4, the inlet and outlet pipes include regenerator hot
所述回热器冷介质板片1.2和回热器热介质板片1.3的相同位置处分布有CO2热侧入口a、CO2冷侧出口b、CO2冷侧入口c和CO2热侧出口d;在回热器前盖板1.1上与回热器冷介质板片1.2和回热器热介质板片 1.3的相同位置处有CO2热侧入口a和CO2冷侧出口b,回热器后盖板1.4 上与回热器冷介质板片1.2和回热器热介质板片1.3的相同位置上有CO2 冷侧入口c和CO2热侧出口d;The CO2 hot side inlet a, CO2 cold side outlet b, CO2 cold side inlet c and CO2 hot side outlet d are distributed at the same position of the regenerator cold medium plate 1.2 and the regenerator heat medium plate 1.3; There are CO2 hot side inlet a and CO2 cold side outlet b at the same position as the regenerator cold medium plate 1.2 and the regenerator hot medium plate 1.3 on the regenerator front cover 1.1, and the regenerator rear cover 1.4 There are CO2 cold side inlet c and CO2 hot side outlet d on the same position as regenerator cold medium plate 1.2 and regenerator heat medium plate 1.3;
所述预冷器热介质板片2.2和预冷器冷介质板片2.3的相同位置上分布有热侧入口e、热水出口f、冷水入口g、热侧出口h;在预冷器前盖板 2.1上与预冷器热介质板片2.2和预冷器冷介质板片2.3的相同位置处有热侧入口e和热水出口f,预冷器后盖板2.4上与预冷器热介质板片2.2和预冷器冷介质板片2.3的相同位置上有冷水入口g和热侧出口h;The hot side inlet e, hot water outlet f, cold water inlet g, and hot side outlet h are distributed on the same position of the precooler heat medium plate 2.2 and the precooler cold medium plate 2.3; on the front cover of the precooler There are hot side inlet e and hot water outlet f on the plate 2.1 at the same position as the precooler heat medium plate 2.2 and the precooler cold medium plate 2.3. The precooler rear cover plate 2.4 is connected to the precooler heat medium. There are cold water inlet g and hot side outlet h on the same position of plate 2.2 and precooler cold medium plate 2.3;
所述回热器热侧入口管道3的一端连接回热器前盖板1.1上的CO2热侧入口a,另一端是外部管道接口,回热器热侧出口-预冷器热侧入口连接管4的一端与回热器后盖板的CO2热侧出口d连接,另一端与预冷器前盖板2.1的热侧入口e连接,预冷器热侧出口管道5与预冷器后盖板2.4 的热侧出口h连接,另一端是外部管道接口,回热器冷侧出口管道6与回热器前盖板1.1上的CO2冷侧出口b连接,另一端是外部管道接口,回热器冷侧入口管道7与回热器后盖板1.4上的CO2冷侧入口c连接,另一端是外部管道接口,冷却水出口管道8与预冷器前盖板上2.1的热水出口f 连接,另一端是外部管道接口,冷却水入口管道9与预冷器后盖板2.4上的冷水入口g连接,另一端是外部管道接口。One end of the regenerator hot
所述回热器冷介质板片1.2和回热器热介质板片1.3以及预冷器热介质板片2.2和预冷器冷介质板片2.3整体程扇形,微通道程辐射状分布于扇面,来回穿梭于不同扇形区域进行换热。The regenerator cold medium plate 1.2, the regenerator heat medium plate 1.3, the precooler heat medium plate 2.2 and the precooler cold medium plate 2.3 are fan-shaped as a whole, and the microchannel paths are radially distributed on the fan surface, Shuttle back and forth between different fan-shaped areas for heat exchange.
所述焊接连接为真空扩散焊连接。The welding connection is a vacuum diffusion welding connection.
所述一种紧凑型多级串联PCHE换热器的换热方法,外部高温CO2 由回热器热侧入口管道3进入回热器热介质板片1.3,释放热量后由回热器热侧出口-预冷器热侧入口连接管4进入预冷器热介质板片2.2,进一步被冷却后由预冷器热侧出口管道5流出换热器供外部设备使用;外部低温 CO2由回热器冷侧入口管道7进入回热器冷介质板片1.2,吸收热量后由回热器冷侧出口管道6流出换热器,供外部设备使用;外部冷却水由冷却水入口管道9进入预冷器冷介质板片2.3,吸收CO2侧热量后由冷却水出口管道8流出换热器外部。The heat exchange method of the compact multi-stage series PCHE heat exchanger, the external high temperature CO2 enters the regenerator heat medium plate 1.3 from the regenerator hot
本发明具有以下有益效果:The present invention has the following beneficial effects:
(1)适合于圆筒形区域布置:本发明在一个圆柱形内集成了回热器和预冷器两个换热器,回热器和预冷器的进出口管道也在圆柱形区域内。这样的布置最大限度的利用了圆柱形空间,满足圆柱形空间布置的特殊需求。(1) It is suitable for the arrangement of the cylindrical area: the present invention integrates two heat exchangers, a regenerator and a precooler in a cylindrical shape, and the inlet and outlet pipes of the regenerator and the precooler are also in the cylindrical area. . Such an arrangement makes the most of the cylindrical space and meets the special needs of the cylindrical space arrangement.
(2)换热器板片整体程扇形,冷端与热端不接触,减小了冷端与热端的直接传热,也减轻了换热器的热应力问题。(2) The overall path of the heat exchanger plate is fan-shaped, and the cold end and the hot end are not in contact, which reduces the direct heat transfer between the cold end and the hot end, and also reduces the thermal stress problem of the heat exchanger.
附图说明Description of drawings
图1为回热器结构分解示意图。Figure 1 is an exploded schematic diagram of the structure of the regenerator.
其中,1.1为回热器前盖板、1.2为回热器冷介质板片、1.3为回热器热介质板片,1.4为回热器后盖板。Among them, 1.1 is the front cover of the regenerator, 1.2 is the cold medium plate of the regenerator, 1.3 is the heat medium plate of the regenerator, and 1.4 is the rear cover of the regenerator.
图2为预冷器结构分解示意图。Figure 2 is a schematic exploded view of the structure of the precooler.
其中,2.1为预冷器前盖板、2.2为预冷器热介质板片、2.3为预冷器冷介质板片,2.4为预冷器后盖板。Among them, 2.1 is the front cover of the precooler, 2.2 is the heat medium plate of the precooler, 2.3 is the cold medium plate of the precooler, and 2.4 is the rear cover of the precooler.
图3为换热器系统整体示意图。FIG. 3 is an overall schematic diagram of the heat exchanger system.
其中,3为回热器热侧入口管道、4为回热器热侧出口-预冷器热侧入口连接管、5为预冷器热侧出口管道、6为回热器冷侧出口管道、7为回热器冷侧入口管道、8为冷却水出口管道、9为冷却水入口管道,Among them, 3 is the inlet pipe of the hot side of the regenerator, 4 is the outlet pipe of the hot side of the regenerator and the inlet of the hot side of the precooler, 5 is the outlet pipe of the hot side of the precooler, 6 is the outlet pipe of the cold side of the regenerator, 7 is the cold side inlet pipe of the regenerator, 8 is the cooling water outlet pipe, 9 is the cooling water inlet pipe,
图4为回热器热介质板片示意图。FIG. 4 is a schematic diagram of the heat medium plate of the regenerator.
图5为回热器冷介质板片示意图。FIG. 5 is a schematic diagram of the cold medium plate of the regenerator.
图6为回热器前盖板示意图。Figure 6 is a schematic diagram of the front cover of the regenerator.
图7为回热器后盖板示意图。FIG. 7 is a schematic diagram of the rear cover plate of the regenerator.
图8为预冷器热介质板片示意图。FIG. 8 is a schematic diagram of a precooler heat medium plate.
图9为预冷器冷介质板片示意图。FIG. 9 is a schematic diagram of the cold medium plate of the precooler.
图10为预冷器前盖板示意图。Figure 10 is a schematic diagram of the front cover of the precooler.
图11为预冷器后盖板示意图。Figure 11 is a schematic diagram of the rear cover of the precooler.
其中,a为CO2热侧入口、b为CO2冷侧出口、c为CO2冷侧入口、 d为CO2热侧出口、e为热侧入口、f为热水出口、g为冷水入口、h为热侧出口。where a is the CO2 hot side inlet, b is the CO2 cold side outlet, c is the CO2 cold side inlet, d is the CO2 hot side outlet, e is the hot side inlet, f is the hot water outlet, g is the cold water inlet, and h is the hot side side exit.
具体实施方式Detailed ways
下面结合附图和具体实施方式对本发明作进一步详细说明。The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.
如图1、图2和图3所示,本发明一种紧凑型多级串联PCHE换热器,所述换热器系统能够实现超临界CO2发电系统中回热器与预冷器的功能,整体呈圆柱状,该系统包括回热器、预冷器、进出口管道及连接管;所述回热器包括从前到后依次焊接连接为整体的回热器前盖板1.1、若干回热器冷介质板片1.2、若干回热器热介质板片1.3和回热器后盖板1.4,所述预冷器包括从前到后依次焊接连接为整体的预冷器前盖板2.1、若干预冷器热介质板片2.2、若干预冷器冷介质板片2.3和预冷器后盖板2.4,所述进出口管道包括回热器热侧入口管道3、预冷器热侧出口管道5、回热器冷侧出口管道6、回热器冷侧入口管道7、冷却水出口管道8和冷却水入口管道9,所述连接管为回热器热侧出口-预冷器热侧入口连接管4,所述回热器和预冷器通过回热器热侧出口-预冷器热侧入口连接管4连接在一起;所述回热器冷介质板片1.2、回热器热介质板片1.3、预冷器热介质板片2.2、预冷器冷介质板片2.3均为金属板面上蚀刻微通道的板片,所述回热器冷介质板片1.2和回热器热介质板片1.3间隔分布,所述预冷器热介质板片2.2和回热器冷介质板片2.3间隔分布。As shown in Figure 1, Figure 2 and Figure 3, a compact multi-stage series PCHE heat exchanger of the present invention, the heat exchanger system can realize the functions of a regenerator and a precooler in a supercritical CO2 power generation system, The whole is cylindrical, and the system includes a regenerator, a precooler, inlet and outlet pipes and connecting pipes; the regenerator includes a regenerator front cover plate 1.1, a number of regenerators, which are welded and connected as a whole from front to back. Cold medium plate 1.2, several regenerator heat medium plates 1.3 and regenerator rear cover plate 1.4, the precooler includes a precooler front cover plate 2.1 welded and connected as a whole from front to back in sequence, a number of precooler Heater heat medium plate 2.2, several precooler cold medium plates 2.3 and precooler rear cover plate 2.4, the inlet and outlet pipes include regenerator hot
如图4、图4、图6和图7,所述回热器冷介质板片1.2和回热器热介质板片1.3的相同位置处分布有CO2热侧入口a、CO2冷侧出口b、CO2 冷侧入口c和CO2热侧出口d;在回热器前盖板1.1上与回热器冷介质板片1.2和回热器热介质板片1.3的相同位置处有CO2热侧入口a和CO2冷侧出口b,回热器后盖板1.4上与回热器冷介质板片1.2和回热器热介质板片1.3的相同位置上有CO2冷侧入口c和CO2热侧出口d。As shown in Figure 4, Figure 4, Figure 6 and Figure 7, the CO2 hot side inlet a, CO2 cold side outlet b, CO2 hot side inlet a, CO2 cold side outlet b, CO2 cold side inlet c and CO2 hot side outlet d; there are CO2 hot side inlets a and CO2 cold side outlet b, there are CO2 cold side inlet c and CO2 hot side outlet d on the same position as the regenerator cold medium plate 1.2 and the regenerator heat medium plate 1.3 on the rear cover plate 1.4 of the regenerator.
如图8、图9、图10和图11所示,所述预冷器热介质板片2.2和预冷器冷介质板片2.3的相同位置上分布有热侧入口e、热水出口f、冷水入口 g、热侧出口h;在预冷器前盖板2.1上与预冷器热介质板片2.2和预冷器冷介质板片2.3的相同位置处有热侧入口e和热水出口f,预冷器后盖板 2.4上与预冷器热介质板片2.2和预冷器冷介质板片2.3的相同位置上有冷水入口g和热侧出口h。As shown in Figure 8, Figure 9, Figure 10 and Figure 11, the hot side inlet e, the hot water outlet f, the hot side inlet e, the hot water outlet f, Cold water inlet g, hot side outlet h; on the front cover plate 2.1 of the precooler, there are hot side inlet e and hot water outlet f at the same position as the precooler heat medium plate 2.2 and the precooler cold medium plate 2.3 , There is a cold water inlet g and a hot side outlet h on the same position of the precooler rear cover plate 2.4 as the precooler heat medium plate 2.2 and the precooler cold medium plate 2.3.
所述回热器热侧入口管道3的一端连接回热器前盖板1.1上的CO2热侧入口a,另一端是外部管道接口,回热器热侧出口-预冷器热侧入口连接管4的一端与回热器后盖板的CO2热侧出口d连接,另一端与预冷器前盖板2.1的热侧入口e连接,预冷器热侧出口管道5与预冷器后盖板2.4 的热侧出口h连接,另一端是外部管道接口,回热器冷侧出口管道6与回热器前盖板1.1上的CO2冷侧出口b连接,另一端是外部管道接口,回热器冷侧入口管道7与回热器后盖板1.4上的CO2冷侧入口c连接,另一端是外部管道接口,冷却水出口管道8与预冷器前盖板上2.1的热水出口f 连接,另一端是外部管道接口,冷却水入口管道9与预冷器后盖板2.4上的冷水入口g连接,另一端是外部管道接口。One end of the regenerator hot
如图4、图5、图8和图9所示,,本发明换热器板片整体程扇形,微通道程辐射状分布于扇面,流体沿箭头方向来回穿梭于不同扇形区域进行换热。As shown in Figure 4, Figure 5, Figure 8 and Figure 9, the heat exchanger plate of the present invention is fan-shaped as a whole, and the micro-channels are radially distributed on the fan surface, and the fluid shuttles back and forth in the direction of the arrow to different fan-shaped areas for heat exchange.
如图3所示,本发明一种紧凑型多级串联PCHE换热器的换热方法,外部高温CO2由回热器热侧入口管道3进入回热器热介质板片1.3,释放热量后由回热器热侧出口-预冷器热侧入口连接管4进入预冷器热介质板片2.2,进一步被冷却后由预冷器热侧出口管道5流出换热器供外部设备使用;外部低温CO2由回热器冷侧入口管道7进入回热器冷介质板片1.2,吸收热量后由回热器冷侧出口管道6流出换热器,供外部设备使用;外部冷却水由冷却水入口管道9进入预冷器冷介质板片2.3,吸收CO2侧热量后由冷却水出口管道8流出换热器外部。As shown in Figure 3, a heat exchange method of a compact multi-stage series PCHE heat exchanger of the present invention, the external high temperature CO2 enters the regenerator heat medium plate 1.3 from the regenerator hot
以上详细说明仅为本发明的较佳实施例,如换热器外部管道供给方向有变化,例如冷却水进出口在换热器后方,只需调整连接管方向即可,不能以此限定本发明的范围。即凡是依据本发明申请范围所作的均等变化与修饰,皆应属于本发明专利涵盖的范围之内。The above detailed description is only a preferred embodiment of the present invention. If the supply direction of the external pipes of the heat exchanger changes, for example, the cooling water inlet and outlet are behind the heat exchanger, it is only necessary to adjust the direction of the connecting pipes, and the present invention cannot be limited by this. range. That is, all equivalent changes and modifications made according to the scope of the application of the present invention shall fall within the scope covered by the patent of the present invention.
Claims (4)
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113155503A (en) * | 2021-04-30 | 2021-07-23 | 武汉理工大学 | Supercritical carbon dioxide heat exchange performance test platform for printed circuit board type heat exchanger |
| CN113335019A (en) * | 2021-06-15 | 2021-09-03 | 东风汽车集团股份有限公司 | Integrated heat exchanger of automobile heat management system |
| WO2023216808A1 (en) * | 2022-05-07 | 2023-11-16 | 西安热工研究院有限公司 | Lead-bismuth supercritical carbon dioxide heat exchange system and method |
| CN117490455A (en) * | 2024-01-02 | 2024-02-02 | 陕西益信伟创智能科技有限公司 | Radiator for printed circuit board |
| EP4273492B1 (en) * | 2022-05-04 | 2025-11-19 | Liebherr-Aerospace Toulouse SAS | Heat exchange device with outer plates having at least one recess, air conditioning system and vehicle |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1419840A (en) * | 1972-11-16 | 1975-12-31 | Avco Corp | Plate type heat exchangers |
| DE2611441A1 (en) * | 1976-03-18 | 1977-09-22 | Schleich Josef | Construction of subterranean section of power station - for waste heat utilisation, using known and new building elements |
| WO1979000766A1 (en) * | 1978-03-15 | 1979-10-04 | Sulzer Ag | Device for heat exchange and manufacturing process thereof |
| CN204514136U (en) * | 2015-04-01 | 2015-07-29 | 安徽理工大学 | A kind of spiral plate type waste heat recycling device |
| CN110686550A (en) * | 2019-11-18 | 2020-01-14 | 西安热工研究院有限公司 | A compact uniform transition interface for printed circuit board heat exchanger and its preparation process |
-
2020
- 2020-07-27 CN CN202010730018.2A patent/CN111721150B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1419840A (en) * | 1972-11-16 | 1975-12-31 | Avco Corp | Plate type heat exchangers |
| DE2611441A1 (en) * | 1976-03-18 | 1977-09-22 | Schleich Josef | Construction of subterranean section of power station - for waste heat utilisation, using known and new building elements |
| WO1979000766A1 (en) * | 1978-03-15 | 1979-10-04 | Sulzer Ag | Device for heat exchange and manufacturing process thereof |
| CN204514136U (en) * | 2015-04-01 | 2015-07-29 | 安徽理工大学 | A kind of spiral plate type waste heat recycling device |
| CN110686550A (en) * | 2019-11-18 | 2020-01-14 | 西安热工研究院有限公司 | A compact uniform transition interface for printed circuit board heat exchanger and its preparation process |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113155503A (en) * | 2021-04-30 | 2021-07-23 | 武汉理工大学 | Supercritical carbon dioxide heat exchange performance test platform for printed circuit board type heat exchanger |
| CN113155503B (en) * | 2021-04-30 | 2024-03-08 | 武汉理工大学 | Supercritical carbon dioxide heat exchange performance test platform for printed circuit board type heat exchanger |
| CN113335019A (en) * | 2021-06-15 | 2021-09-03 | 东风汽车集团股份有限公司 | Integrated heat exchanger of automobile heat management system |
| CN113335019B (en) * | 2021-06-15 | 2022-09-30 | 东风汽车集团股份有限公司 | Integrated heat exchanger of automobile heat management system |
| EP4273492B1 (en) * | 2022-05-04 | 2025-11-19 | Liebherr-Aerospace Toulouse SAS | Heat exchange device with outer plates having at least one recess, air conditioning system and vehicle |
| WO2023216808A1 (en) * | 2022-05-07 | 2023-11-16 | 西安热工研究院有限公司 | Lead-bismuth supercritical carbon dioxide heat exchange system and method |
| CN117490455A (en) * | 2024-01-02 | 2024-02-02 | 陕西益信伟创智能科技有限公司 | Radiator for printed circuit board |
| CN117490455B (en) * | 2024-01-02 | 2024-03-15 | 陕西益信伟创智能科技有限公司 | Radiator for printed circuit board |
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